WO2014169122A1 - Dispositif de stockage d'énergie aqueuse avec des matériaux d'électrodes organiques - Google Patents

Dispositif de stockage d'énergie aqueuse avec des matériaux d'électrodes organiques Download PDF

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WO2014169122A1
WO2014169122A1 PCT/US2014/033652 US2014033652W WO2014169122A1 WO 2014169122 A1 WO2014169122 A1 WO 2014169122A1 US 2014033652 W US2014033652 W US 2014033652W WO 2014169122 A1 WO2014169122 A1 WO 2014169122A1
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electrode
organic
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battery
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Yan YAO
Yanliang LIANG
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University of Houston System
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University of Houston System
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Priority to KR1020177023664A priority Critical patent/KR20170106465A/ko
Priority to CN201480028911.3A priority patent/CN106463781B/zh
Priority to KR1020157031865A priority patent/KR20150139944A/ko
Priority to EP14783178.8A priority patent/EP2984698B1/fr
Priority to JP2016507659A priority patent/JP6490664B2/ja
Priority to KR1020187019594A priority patent/KR102214862B1/ko
Publication of WO2014169122A1 publication Critical patent/WO2014169122A1/fr
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/60—Selection of substances as active materials, active masses, active liquids of organic compounds
    • H01M4/602—Polymers
    • H01M4/606—Polymers containing aromatic main chain polymers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/24—Alkaline accumulators
    • H01M10/28—Construction or manufacture
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/60—Selection of substances as active materials, active masses, active liquids of organic compounds
    • H01M4/602—Polymers
    • H01M4/606—Polymers containing aromatic main chain polymers
    • H01M4/608—Polymers containing aromatic main chain polymers containing heterocyclic rings
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00—Electrolytes
    • H01M2300/0017—Non-aqueous electrolytes
    • H01M2300/002—Inorganic electrolyte
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49002—Electrical device making
    • Y10T29/49108—Electric battery cell making

Definitions

  • This disclosure relates to a secondary or rechargeable battery, specifically to a battery with an aqueous electrolyte and at least one organic material used for an electrode.
  • aqueous metal-ion batteries represent a potential improvement in battery technology for commercial and industrial applications, particularly in vehicular designs.
  • Prototype aqueous batteries have previously demonstrated -75 Wh kg of energy density based on the weight of electrodes.
  • this parameter remains below the effective specific energy densities required to meet various governmental and regulatory recommended metrics, as well as certain application-specific demands.
  • cathode materials employed in some non-aqueous lithium-ion batteries (LIBs) are generally stable in aqueous electrolytes.
  • Exemplary lithium-based cathode materials such as layered L1C0O 2 and spinel LiM ⁇ C have shown capacities approaching their theoretical values with good reversibility at high charge/discharge rates.
  • the intercalation compound-based anodes have demonstrated unsatisfactory cyclability in AMIBs, including aqueous lithium ion batteries (ALIB), due to material dissolution into the bulk electrolyte and oxidation by O 2 at the discharged state.
  • ALOB aqueous lithium ion batteries
  • creating an anode material with satisfactory cyclability for operation in high energy density batteries represents a technological hurdle to commercial implementation of AMIBs as a whole.
  • the disclosure includes an AMIB having at least one electrode comprising at least one organic electrode material, wherein the organic electrode material comprises an organic electroactive compound. Further disclosed is an AMIB comprising a first electrode comprising at least one organic electrode material, an aqueous electrolyte, and a second electrode capable of metal-ion (de)intercalation/(un-)coordination.
  • the first electrode comprises at least one organic electrode material chosen from carbonyl compounds.
  • a method of constructing an aqueous battery comprising preparing an electrode capable of metal-ion (de)intercalation/(un-)coordination, contacting the electrode capable of metal-ion (de)intercalation/(un-)coordination with an aqueous electrolyte, preparing an electrode comprising at least one organic electrode material, contacting the electrode comprising at least one organic electrode material with the aqueous electrolyte, and applying an electric current to the two electrodes.
  • the electrode comprising at least one organic electrode material comprises one or a mixture of organic electrode materials bearing electroactive carbonyl groups.
  • FIGURE 1 illustrates representative molecular structures of the organic electrode materials (OEMs) for implementation as electrode materials for an AMIB;
  • FIGURE 2 illustrates O2/H2 evolution potential of water as a function of pH as compared to the potential and capacity of state-of-the-art anode materials for ALIBs (on the left) and the disclosed organic carbonyl compounds (OCCs) (on the right);
  • FIGURE 3 illustrates molecular structures of exemplary OEMs
  • FIGURE 4 illustrates the charge-discharge profile of PAQS in a 2.0 M Li 2 S0 4 aqueous solution at pH 14 measured in a three-electrode cell at a rate for charge and discharge of 1C (Coulomb);
  • FIGURE 6 illustrates the cycling performance of PAQS in a 2.0 M TEAC1 aqueous solution at pH 14 at a rate for charge and discharge of 1C
  • FIGURE 7 illustrates the charge-discharge profile of PBDTD in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell at a rate for charge and discharge of 1C;
  • FIGURE 8 illustrates the cycling performance of PBDTD in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 at a rate for charge and discharge of 1C;
  • FIGURE 9 illustrates the charge-discharge profile of a full cell comprising PBDTD as the anode and LiMn 2 0 4 as the cathode with a 2.5 M Li 2 S0 4 aqueous solution (pH 7) as the electrolyte at a rate for charge and discharge of 1C;
  • FIGURE 11 illustrates the rate capability of PBDTD in a 2.5 M Li 2 S0 4 aqueous solution at pH 7at the same rate for both charge and discharge;
  • FIGURE 12 illustrates the charge-discharge profile of PBDTDS in a 2.5 M Li 2 S0 4 aqueous solution at pH 13 measured in a three-electrode cell at a rate for charge and discharge of 1C;
  • FIGURE 13 illustrates the rate capability of PBDTDS in a 2.5 M Li 2 S0 4 aqueous solution at pH 13 at the same rate for both charge and discharge;
  • FIGURE 14 illustrates the cycling performance of PBDTDS in a 2.5 M Li 2 S0 4 aqueous solution at pH 13 at a rate for charge and discharge of IOC;
  • FIGURE 15 illustrates the charge-discharge profile of a full cell comprising PBDTDS as the anode and LiCo0 2 as the cathode with a 2.5 M Li 2 S0 4 aqueous solution (pH 13) as the electrolyte at a rate for charge and discharge of 5C;
  • FIGURE 17 illustrates the charge-discharge profile of PBFFD in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell at a rate for charge and discharge of 1C;
  • FIGURE 18 illustrates the charge-discharge profile of PBFFDS in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell at a rate for charge and discharge of 1C;
  • FIGURE 19 illustrates the charge-discharge profile of PPQ in a 2.5 M Li 2 S0 4 aqueous solution at pH 13 measured in a three-electrode cell at a rate for charge and discharge of 1C;
  • FIGURE 20 illustrates the cycling performance of PPQ in a 2.5 M Li 2 S0 4 aqueous solution at pH 13 at a rate for charge and discharge of 1C;
  • FIGURE 21 illustrates the charge-discharge profile of PPTO in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell. Rate for charge and discharge: 1C;
  • FIGURE 22 illustrates the charge-discharge profile of PNDI in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell. Rate for charge and discharge: 1C;
  • FIGURE 23 illustrates the charge-discharge profile of PNDIE in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell. Rate for charge and discharge: 1C;
  • FIGURE 24 illustrates the rate capability of PNDIE in a 2.5 M Li 2 S0 4 aqueous solution at pH 7. Same rate for both charge and discharge;
  • FIGURE 25 illustrates the cycling performance of PNDIE in a 2.5 M Li 2 S0 4 aqueous solution at pH 7. Rate for charge and discharge: IOC;
  • FIGURE 27 illustrates the charge-discharge profile of PNDIB in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell. Rate for charge and discharge: 1C;
  • FIGURE 28 illustrates the charge-discharge profile of PPDIE in a 2.5 M Li 2 S0 4 aqueous solution at pH 7 measured in a three-electrode cell. Rate for charge and discharge: 1C.
  • electrical energy storage devices include capacitors and batteries. While both have various applications, batteries are preferred in the computer and electric vehicle industries for their cyclability and energy/power density. Batteries and particularly secondary or rechargeable batteries are configured as one or more electrochemical cells capable of converting electrical energy into chemical energy during charging and converting chemical energy into electric energy during discharging. In operation of most conventional batteries, the cathode and anode undergo compositional changes during discharging that are restored during charging. The medium through which the electrodes are electrically coupled is the electrolyte. Currently, solutions of salts, bases, and acids in aqueous/non-aqueous solvents are used as electrolytes in secondary batteries.
  • Aqueous electrolyte batteries may provide design options that are not available in organic electrolyte-based battery configurations, such as but not limited to LIBs. More specifically, AMIBs have improved safety and flexibility in vehicle design at reduced system costs compared to LIBs because AMIBs including aqueous lithium-ion batteries (ALIB) use the highly reversible ion-intercalation principle of conventional LIBs but with lower-cost, nonflammable aqueous electrolytes.
  • ALOB aqueous lithium-ion batteries
  • the present disclosure relates to battery configurations including at least one electrode comprising OEMs including but not limited to, OCCs.
  • OEMs of the present disclosure are configurable to operate as both the anode and cathode or to couple with existing cathodic and anodic materials, including but not limited to lithium mixed oxides.
  • the OEM applications in AMIBs demonstrate inorganic and organic hybrid redox couples. As disclosed herein, these redox couples appear to satisfy certain technical performance targets for energy density both in weight and in volume. Further, these properties are maintained in AMIB configurations comprising at least one organic electrode.
  • organic electrode AMIB configurations disclosed herein represent an additional reduction in the cost of producing a battery, without reduction in eye lability and energy/power density.
  • Figure 1 illustrates representative molecular structures of the exemplary OEMs for implementation as electrode materials for an AMIB.
  • OCCs are used as the anodic material for an AMIB.
  • Suitable OCCs comprise at least one structural formula illustrated in Figure 1.
  • the three structural formulas comprise (I) structures where electroactive cores are attached to a poly -/oligomer segment, (II) structures where electroactive cores are linked with linkers in-between, and (III) structures where electroactive cores are directly connected to one another.
  • the core comprises carbonyl group.
  • the chain comprises any polymer or oligomer.
  • L comprises a moiety chosen from the group consisting of dicarbonyl, NH, O, S, CH 2 , (CH 2 ) 2 , (CH 2 )3, (CH 2 ) 4 , (CH2)6, optionally substituted 5-6 membered aryl/heteroaryl groups, and biaryls consisted of two identical or different optionally substituted 5-6 membered aryl/heteroaryl groups.
  • "n" indicates the average number of repeating units in the formula. The average number of repeats is at least 2.
  • Figure 1 likewise illustrates exemplary core structures (a) through (m) that fit within the three OCC structural formulas (I)— (III).
  • Ar 1 comprises at least one moiety chosen from the group consisting of naphthalene, perylene, optionally substituted 5-6 membered aryl/heteroaryl groups, and biaryls consisted of two identical or different optionally substituted 5-6 membered aryl/heteroaryl groups.
  • R comprises at least one moiety chosen from H, CH 3 , or C2H5.
  • OCCs are generally insoluble even at the reduced state and show stable capacity retention in both organic and aqueous electrolytes.
  • the employed electroactive moieties without limitation include 1 ,4-benzoquinone, 1,2-benzoquinone, 1,2-bicarbonyl, diimide, and their derivatives.
  • Aromatic rings can be incorporated to fine-tune the properties of the OCCs.
  • the structural variety and design strategy of organic compounds permit predictable tuning of their redox potential in a wide range in order to fulfill specific device requirements.
  • the reduced form of these structures coordinated to metal-ions, which are prepared via (electro)chemical reduction or formed in situ during charge-discharge, are also within the scope of the disclosure.
  • the disclosed OCCs can demonstrate the characteristics for implementation as electrode materials for ALIBs. As noted hereinabove, these OEMs are merely representative and related configurations of the OEMs are considered within the scope of the present disclosure.
  • ORGANIC ELECTRODE POTENTIALS Referring now to Figure 2, the 0 2 /H 2 evolution potential of an exemplary aqueous electrolyte model, in this case water, as a function of pH is illustrated. More specifically, the thermodynamic stability of water is illustrated by solid lines and the dashed lines show the kinetic stability range for aqueous electrolytes considering the over-potentials for gas evolution.
  • the organic electrode materials are selected and configured to have a potential within the range of the kinetic stability, including the gas evolution over-potentials, at a pH 7.
  • OCCs include anthraquinone (AQ), benzofuro[5,6-Z?]furan-4,8-dione (BFFD), 2,5-dimethoxy-l,4-benzoquinone (DMBQ), poly(2,5-dihydroxy-l,4-benzoquinonyl sulfide (PDBS), poly(pyromellitic diimide) (PI), 5,7, 12,14-pentacenetetrone (PT), and pyrene- 4,5,9, 10-tetraone (PTO), without limitation.
  • AQ anthraquinone
  • BFFD benzofuro[5,6-Z?]furan-4,8-dione
  • DMBQ 2,5-dimethoxy-l,4-benzoquinone
  • PDBS poly(2,5-dihydroxy-l,4-benzoquinonyl sulfide
  • PI poly(pyromellitic diimide)
  • PT pyrene- 4,5
  • metal oxide electrodes exhibit specific capacities that do not exceed 200 mAh/g.
  • the metal oxide electrodes are conventionally found in ALIBs.
  • the specific capacities of the OEMs are greater than 200 mAh/g.
  • the exemplary OEMs include the previously discussed OCCs.
  • a battery configured with the OEMs disclosed herein provides a method of increasing the specific capacity of a battery.
  • the OEM electrodes are fabricated by coating a support with a mixture containing at least one OEM. Generally, the mixture is coated onto a support and pressed and/or dried to form the electrode. Alternatively, the mixture may be compressed in contact with a foil, foam, or mesh. More specifically, the mixture comprises a dispersion of at least one OEM, conductive carbon, and at least one fluoropolymer. In certain configurations, the mixture comprises a polar solvent such as but not limited to N- methyl-2-pyrrolidone (NMP), ethanol, and isopropanol.
  • NMP N- methyl-2-pyrrolidone
  • the mixture comprises a dispersion of OEM, conductive carbon, and a fluoropolymer.
  • concentration of the OEM is between about 20 wt.% and about 90 wt.%, and in certain configurations between about 30 wt.% and about 80 wt.%.
  • the conductive carbon concentration is between about 5 wt.% and about 75 wt.%, and in certain configurations between about 10 wt.% and about 60 wt.%.
  • the fluorpolymer concentration is between about 1 wt.% and about 30 wt.% and in certain configurations between about 5 wt.% and about 25 wt.%.
  • the fluoropolymer may comprise at least one chosen from polyvinylidene fluoride (PVDF) and polytetrafluoroethylene (PTFE).
  • the support is configured to be a current collector.
  • current collectors comprise a metallic foam, foil, or mesh.
  • the metal of the foam, foil, or mesh comprises at least one transition metal, including Group VIB, VIIB, VIII, IB, IIB, and IIIA metals.
  • the foam, foil, or mesh comprises a Group VIII metal, such as but not limited to nickel (Ni); alternatively, the foam, foil, or mesh comprises a Group IIIA metal such as but not limited to aluminum (Al).
  • the foam, foil, or mesh may be coated by a second metal chosen from the transition metal groups listed hereinabove.
  • the second metal is a Group VIII metal, such as but not limited to nickel (Ni).
  • the foam, foil, or mesh may comprise stainless steel.
  • the mixture coats the support and is pressed and/or dried to form the OEM electrode.
  • the mixture may be forced into the support prior to drying.
  • pressure is used to force the mixture into the foam or mesh supports.
  • the pressure comprises mixture injections, compression of the mesh or foam, and the compression of mesh or foam loaded with the (dried) mixture. Pressure may include 0.3-2.0 MPa without limitation.
  • the disclosed electrode materials are configurable for implementation in AMIBs.
  • the batteries comprise an electrode capable of intercalation by/coordination to at least one metal-ion chosen from the group comprising lithium (Li), sodium (Na), magnesium (Mg), calcium (Ca), and in certain instances aluminum (Al).
  • the batteries configured thusly use a group of electrochemical redox couples that leverage metal-ion battery electrode chemistry characteristics to potentially provide a reliable and high capacity electrode material to meet certain technical performance parameters for AMIBs in commercial applications.
  • Counter electrodes containing compounds capable of metal-ion (de)intercalation/(un-)coordination may be utilized. Generally, the counter electrodes comprise between about 50 wt.% and about 100 wt.% of compounds capable of metal-ion (de)intercalation/(un-)coordination; alternatively the counter electrodes comprise between about 60 wt.% and about 95 wt.% metal-containing compounds.
  • non-limiting exemplary compounds capable of metal-ion (de)intercalation/(un-)coordination include L1C0O2, Li ii/3Coi/3Mni/ 3 02, LiNio.8Coo.15Alo.05O2, lithium-rich mixed oxides, LiNio.5Mn1.5O4 Ni(OH) 2 , Mn02, carbonyl compounds, organosulfur compounds, radical compounds, non-conjugated polymers, and combinations thereof.
  • the counter-electrodes are fabricated in a mixture method as described hereinabove.
  • the disclosed batteries uses a group of electrochemical redox couples that leverage lithium-ion battery cathode chemistry characteristics to potentially provide a reliable and high capacity anode material to meet certain technical performance parameters for ALIBs in commercial applications.
  • Certain exemplary OEMs that are sustainable, low-cost, and high-energy are illustrated in Figure 3.
  • One exemplary electrochemical redox couple of LiM ⁇ O PAQS has the following reactions illustrated in Equation 1 [EQ 1] and Equation 2 [EQ 2].
  • LiMn 2 0 4 ⁇ Lii_ x Mn 2 0 4 + xLi + + jce " ( ⁇ 1.0 V vs. Ag/AgCl)
  • the aqueous electrolytes are composed of at least one metal salt as solute and an aqueous solvent which comprises at least 90 wt.% of water.
  • the aqueous electrolytes may have a pH between about pH 2 and about pH 15.
  • the aqueous electrolytes may have a pH between about pH 6 and about pH 14.
  • the electrolytes may be chosen to most stably support the operation of the electrodes, including a cathode capable of metal-ion (de)intercalation/(un-)coordination and an OEM electrode.
  • the disclosed OEMs may be incorporated into an AMIB such that special protection is unneeded in commercial applications, including vehicular and industrial applications.
  • the battery configurations are multifunctional. Relating to the stability of the OEMs and the tunability of the electrolytes in the secondary or rechargeable, aqueous, metal-ion battery, the battery may be configurable as a structural member. Exemplary structural members may comprise frames, supports, trusses, chassis, or other components of electrical and mechanical equipment.
  • Example 1 PAQS (see Figure 3a) A mixture of PAQS (70 wt.%), Super-P carbon (20 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L1 2 SO 4 (2.0 M) and LiOH (1.0 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.80 V vs Ag/AgCl ( Figure 4).
  • PAQS delivers reversible cycling performance when working in sodium (2.0 M NaCl + 1.0 M NaOH)/potassium (2.0 M KC1 + 1.0 M KOH) salt-based electrolytes (Figure 5).
  • TEA tetraethylammonium
  • Figure 6 A lower capacity was obtained when a neutral lithium salt-based electrolyte (2.5 M L1 2 SO 4 ) was used.
  • Example 2 PBDTD (see Figure 3b) A mixture of PBDTD (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.45 V vs Ag/AgCl ( Figure 7). Rate performance tested in two-electrode coin cells showed a 93% capacity retention at IOC compared to that obtained at 1C ( Figure 8).
  • Example 3 PBDTDS (see Figure 3c) PBDTDS was synthesized with a similar method as that for PAQS. A mixture of PBDTDS (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L1 2 SO 4 (2.5 M) and LiOH (0.1 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.42 V vs Ag/AgCl ( Figure 12).
  • Rate performance tested in two-electrode coin cells showed 91 % and 60% of capacity retention at IOC and lOOC, respectively ( Figure 13). At IOC rate (for both charge and discharge), 93% of the original capacity was maintained after 2000 cycles ( Figure 14). Alternatively, a mixture of L1C0O 2 (80 wt.%), Super-P carbon (10 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the counter electrode. Coin cells are fabricated to demonstrate an average discharge potential of 0.96 V ( Figure 15). When a neutral electrolyte was used, a lower capacity was obtained (Figure 16).
  • Example 4 PBFFD (see Figure 3d) PBFFD was synthesized with a similar method as that for PBDTD. A mixture of PBFFD (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L1 2 SO 4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.38 V vs Ag/AgCl ( Figure 17).
  • Example 5 PBFFDS (see Figure 3e) PBFFDS was synthesized with a similar method as that for PAQS. A mixture of PBFFDS (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L1 2 SO 4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.34 V vs Ag/AgCl ( Figure 18).
  • Example 6 PPQ (see Figure 3f) PPQ was synthesized with a similar method as that for PBDTD. A mixture of PPQ (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L1 2 SO 4 (2.5 M) of LiOH (0.1 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.45 V vs Ag/AgCl ( Figure 19). At 1C rate (for both charge and discharge), no capacity degradation was observed after 200 cycles ( Figure 20).
  • Example 7 PPTO (see Figure 3g) PPTO was synthesized with a similar method as that for PBDTD. A mixture of PPTO (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.46 V vs Ag/AgCl ( Figure 21).
  • Example 8 PNDI (see Figure 3h) A mixture of PNDI (30 wt.%), Super-P carbon (60 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.44 V vs Ag/AgCl ( Figure 22).
  • Example 9 PNDIE (see Figure 3i) A mixture of PNDIE (60 wt.%), Super-P carbon (30 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.56 V vs Ag/AgCl ( Figure 23). Rate performance tested in two-electrode coin cells showed a 84 % capacity retention at IOC compared to that obtained at 1C ( Figure 24).
  • PNDIE also delivered stable cycling performance when working in sodium (5 M NaN03)/magnesium (2.5 M Mg(N03)2) salt-based electrolytes ( Figure 26).
  • Example 10 PNDIB (see Figure 3j) A mixture of PNDIB (60 wt.%), Super-P carbon (30 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.55 V vs Ag/AgCl ( Figure 27).
  • Example 11 PPDIE (see Figure 3k) A mixture of PPDIE (60 wt.%), Super-P carbon (30 wt.%), and polytetrafluoroethylene (10 wt.%) was pressed into a stainless steel mesh to form the working electrode. A glass fiber paper wet with an aqueous solution of L12SO4 (2.5 M) is placed between the working electrode and a piece of activated carbon cloth serving as the counter electrode. Three-electrode coin cells are fabricated to demonstrate an average reduction potential of -0.79 V vs Ag/AgCl ( Figure 28).
  • R R u +k* (R u -Ri), wherein k is a variable ranging from 1 percent to 100 percent with a 1 percent increment, i.e., k is 1 percent, 2 percent, 3 percent, 4 percent, 5 percent, 50 percent, 51 percent, 52 percent... 95 percent, 96 percent, 97 percent, 98 percent, 99 percent, or 100 percent.
  • any numerical range defined by two R numbers as defined in the above is also specifically disclosed.

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  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
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Abstract

La présente invention concerne une batterie métal-ion aqueux et son procédé de construction. Selon un mode de réalisation, la batterie comporte un électrolyte aqueux et au moins une électrode comportant au moins un matériau d'électrode organique. Le procédé comprend l'incorporation d'un matériau d'électrode organique dans l'électrode d'une batterie métal-ion aqueux. Le matériau d'électrode organique comporte également au moins un matériau choisi parmi des composés carbonylés.
PCT/US2014/033652 2013-04-10 2014-04-10 Dispositif de stockage d'énergie aqueuse avec des matériaux d'électrodes organiques Ceased WO2014169122A1 (fr)

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KR1020177023664A KR20170106465A (ko) 2013-04-10 2014-04-10 유기 전극 물질을 가지는 수성 에너지 저장 장치
CN201480028911.3A CN106463781B (zh) 2013-04-10 2014-04-10 具有有机电极材料的水性能量存储装置
KR1020157031865A KR20150139944A (ko) 2013-04-10 2014-04-10 유기 전극 물질을 가지는 수성 에너지 저장 장치
EP14783178.8A EP2984698B1 (fr) 2013-04-10 2014-04-10 Dispositif de stockage d'énergie aqueuse avec des matériaux d'électrodes organiques
JP2016507659A JP6490664B2 (ja) 2013-04-10 2014-04-10 有機電極材料を用いた水溶液系エネルギー貯蔵装置
KR1020187019594A KR102214862B1 (ko) 2013-04-10 2014-04-10 유기 전극 물질을 가지는 수성 에너지 저장 장치

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US10522875B2 (en) 2015-05-22 2019-12-31 University Of Houston System Lead-acid batteries with fast charge acceptance
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US20140308581A1 (en) 2014-10-16
KR20170106465A (ko) 2017-09-20
EP2984698A1 (fr) 2016-02-17
JP2016514897A (ja) 2016-05-23
EP2984698A4 (fr) 2016-12-14
CN106463781A (zh) 2017-02-22
KR102214862B1 (ko) 2021-02-09
US10411262B2 (en) 2019-09-10
KR20180081185A (ko) 2018-07-13
EP2984698B1 (fr) 2022-07-13
KR20150139944A (ko) 2015-12-14
JP6490664B2 (ja) 2019-03-27

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